JPH06134207A - Oil-water separation device - Google Patents

Oil-water separation device

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Publication number
JPH06134207A
JPH06134207A JP28889792A JP28889792A JPH06134207A JP H06134207 A JPH06134207 A JP H06134207A JP 28889792 A JP28889792 A JP 28889792A JP 28889792 A JP28889792 A JP 28889792A JP H06134207 A JPH06134207 A JP H06134207A
Authority
JP
Japan
Prior art keywords
separation
tank
oil
water
fat
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP28889792A
Other languages
Japanese (ja)
Other versions
JP2580449B2 (en
Inventor
Shoji Ikemoto
正二 池本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SANITARII KK
Original Assignee
SANITARII KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SANITARII KK filed Critical SANITARII KK
Priority to JP4288897A priority Critical patent/JP2580449B2/en
Publication of JPH06134207A publication Critical patent/JPH06134207A/en
Application granted granted Critical
Publication of JP2580449B2 publication Critical patent/JP2580449B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To separate waste water efficiently into a fatty oil component and water by providing a fat and oil returning pipe for returning the fat and oil component separated and floated to the side of a separation inner tank in a precipitation separation tank. CONSTITUTION:A separation tank (2) of double structure body locating a separation inner tank (6) with a lower side opening (5) is disposed inside a separation outer tank (4) with a bottom (3) formed into the tank shape and waste water (A) mixed with animal or vegetable oil is fed to the side side of the separation inner tank 6 of the separation tank (2), and separated into the fat and oil component, primary intermediate water (D) and slurry. A mixing device (19) for injecting a neutralizing agent (E) such as caustic side into the primary intermediate water (D) fed out from the side of the separation outer tank (4) and mixing therein is provided, and also a precipitation separation tank (30) for separating flocculating intermediate water (A-1) mixed with the neutralizing agent (E) into the fat and oil component and pure water is disposed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はレストランなどより排出
される廃水を油成分と水とに分離する油水分離装置に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an oil / water separation device for separating waste water discharged from a restaurant or the like into oil components and water.

【0002】[0002]

【従来の技術】従来、レストランなどより排出される廃
水には動植物油が混入されており、同廃水は、沈澱槽を
有する分離槽で油成分と水とを分離するものであった。
2. Description of the Related Art Conventionally, animal and vegetable oils have been mixed in the waste water discharged from restaurants and the like, and the waste water is used to separate oil components and water in a separation tank having a settling tank.

【0003】また、同廃水は、沈澱槽に溜めた状態で中
和剤を混合させて処理するものであった。
Further, the waste water is treated by mixing a neutralizing agent in a state of being stored in a settling tank.

【0004】[0004]

【発明が解決しようとする課題】ところが、上記従来例
においては、沈澱槽内において、不純物が沈澱するまで
時間をおく必要があるために装置全体を間歇運転してい
た。したがって、廃水の分離が量的及び質的に低く、ま
た、作業を能率的にできなかった。
However, in the above-mentioned conventional example, the entire apparatus is intermittently operated because it is necessary to wait for the impurities to settle in the settling tank. Therefore, the separation of wastewater was low in quantity and quality, and the work could not be performed efficiently.

【0005】[0005]

【課題を解決するための手段】本発明では、底部を有し
タンク状に形成され分離外槽の内部に、下側開口部を有
する分離内槽を位置させて二重構造とした分離槽を設け
て、同分離槽の分離内槽側に、動植物油が混入された廃
水を供給して、油脂成分と一次中間水及び汚泥とに分離
可能とし、かつ、分離外槽側より取り出した一次中間水
に苛性ソーダなどの中和剤を注入混合する混和装置を設
けると共に、中和剤が混合された凝集中間水を油脂成分
と浄水とに分離する沈澱分離槽を設け、しかも、同沈澱
分離槽には、分離浮上した油脂成分を、分離内槽側へ返
送する油脂戻し管を具備せしめていることを特徴とする
油水分離装置を提供せんとするものである。
According to the present invention, there is provided a separation tank having a double structure in which a separation inner tank having a bottom portion and formed in a tank shape and having a lower opening is located inside the separation outer tank. The waste water mixed with animal and vegetable oils is supplied to the separation inner tank side of the separation tank so that it can be separated into oil and fat components and primary intermediate water and sludge, and the primary intermediate taken out from the separation outer tank side. A mixing device for injecting and mixing a neutralizing agent such as caustic soda into water is provided, and a precipitation separating tank for separating the coagulated intermediate water mixed with the neutralizing agent into oil and fat components and purified water is also provided. The present invention provides an oil / water separation device characterized in that it is equipped with an oil / fat return pipe for returning the oil / fat components that have been separated and floated to the separation inner tank side.

【0006】[0006]

【実施例】本発明の実施例を図面に基づき具体的に説明
すると、1はレストランなどより排出される廃水Aを浄
水Bと、油脂成分及び汚泥などの不純物Cとに分離する
油水分離装置である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described in detail with reference to the drawings. 1 is an oil / water separation device for separating waste water A discharged from a restaurant or the like into purified water B and impurities C such as fat and oil components and sludge. is there.

【0007】2は分離槽であって、同分離槽2は、底部
3を有しタンク状に形成された分離外槽4の内部に、下
側開口部5を有する分離内槽6を位置させて二重構造と
している。そして、同分離槽2の上部には、分離内槽6
の内室6-1 に廃水Aを導入する流入管7を設けている。
Reference numeral 2 denotes a separation tank. In the separation tank 2, a separation inner tank 6 having a lower opening 5 is located inside a separation outer tank 4 having a bottom 3 and formed in a tank shape. Has a double structure. Then, in the upper part of the separation tank 2, a separation inner tank 6
An inflow pipe 7 for introducing the wastewater A is provided in the inner chamber 6-1 of the.

【0008】また、流入管7の基端には、廃水投入口に
廃水Aを投入するポンプ手段8を設けている。9は分離
内槽6の内部で中間位置に設置するヒーター、10は二重
構造となっている分離槽2の分離外槽4と分離内槽6と
の間に形成された外室であって、分離内槽6により分離
された一次中間水Dが貯溜される。
Further, at the base end of the inflow pipe 7, there is provided pump means 8 for introducing the wastewater A into the wastewater inlet. Reference numeral 9 denotes a heater installed at an intermediate position inside the separation inner tank 6, and 10 denotes an outer chamber formed between the separation outer tank 4 and the separation inner tank 6 of the separation tank 2 having a double structure. The primary intermediate water D separated by the separation inner tank 6 is stored.

【0009】11は分離外槽4の底部に設ける汚泥物排出
パイプ、12は分離内槽6の上部位置より外部に向けて水
平状に突設した油脂取出管、13は油脂取出管12の先端に
接続され、かつ、微細目状スクリーン14を有する濾過
槽、15は濾過槽13に接続する油脂貯溜槽であって、ヒー
ター16及び汚泥物排水パイプ17を設置している。
Reference numeral 11 denotes a sludge discharge pipe provided at the bottom of the separation outer tank 4, 12 denotes an oil / fat take-out tube projecting horizontally from an upper position of the separation inner tank 6 to the outside, and 13 denotes a tip of the oil / fat take-out tube 12. Is a filtration tank having a fine screen 14, and 15 is an oil and fat storage tank connected to the filtration tank 13, and is provided with a heater 16 and a sludge drain pipe 17.

【0010】18は分離外槽4の外室10より一次中間水D
を取出す取出口であって、中和剤などを混合する混和装
置19に接続している。
18 is the primary intermediate water D from the outer chamber 10 of the separation outer tank 4.
It is an outlet for taking out and is connected to a mixing device 19 for mixing a neutralizing agent and the like.

【0011】20は苛性ソーダなどの中和剤Eを容れた中
和剤槽で、中和剤Eはパイプ21及び定量ポンプ22により
混和装置19側へ送るようにしている。23は撹拌機、24は
パック等の凝集剤Fを収納した凝集剤槽であって、凝集
剤Fは、パイプ25及び定量ポンプ26により混和装置19側
へ送られる。
Reference numeral 20 denotes a neutralizer tank containing a neutralizer E such as caustic soda, and the neutralizer E is sent to the mixing device 19 side by a pipe 21 and a metering pump 22. Reference numeral 23 is a stirrer, and 24 is a flocculant tank containing a flocculant F such as a pack. The flocculant F is sent to the mixing device 19 side by a pipe 25 and a metering pump 26.

【0012】27は凝集補助剤Gを収納した凝集補助剤槽
であって、上記と同様に凝集補助剤Gはパイプ28と定量
ポンプ29により混和装置19側へ送られる。
Reference numeral 27 denotes a coagulation auxiliary agent tank containing a coagulation auxiliary agent G, and the coagulation auxiliary agent G is sent to the mixing device 19 side by a pipe 28 and a metering pump 29 in the same manner as described above.

【0013】30は沈澱分離槽であって、同沈澱分離槽30
は、沈澱分離外槽31の内部に沈澱分離内槽32を位置させ
て二重構造としている。19A は混和装置19から排出され
る凝集中間水A-1 を沈澱分離槽30内に導く供給パイプ、
33は沈澱分離内槽32の下側開口部、34は沈澱分離外槽31
と沈澱分離内槽32との間に形成された外室であって、沈
澱分離内槽32により分離された二次中間水Hが貯溜され
る。35は沈澱分離外槽31の底部に設ける汚泥物排出パイ
プ、36は沈澱分離内槽32の内部側の上部位置37と、前記
分離内槽6の内部とを接続する油脂戻し管であって、同
油脂戻し管36により沈澱分離内槽32内に溜った油脂成分
などを分離内槽6に向けて排出することができる。
Reference numeral 30 is a precipitation separation tank, and the precipitation separation tank 30
Has a double structure in which the precipitation separation inner tank 32 is located inside the precipitation separation outer tank 31. 19A is a supply pipe for guiding the coagulated intermediate water A-1 discharged from the mixing device 19 into the precipitation separation tank 30,
33 is the lower opening of the precipitation separation inner tank 32, and 34 is the precipitation separation outer tank 31.
The secondary intermediate water H, which is an outer chamber formed between the inner tank 32 and the precipitation separation inner tank 32 and separated by the precipitation separation inner tank 32, is stored. Reference numeral 35 is a sludge discharge pipe provided at the bottom of the precipitation separation outer tank 31, 36 is an oil return pipe connecting the upper position 37 on the inner side of the precipitation separation inner tank 32 and the inside of the separation inner tank 6. By the oil / fat return pipe 36, the oil / fat components accumulated in the precipitation separation inner tank 32 can be discharged toward the separation inner tank 6.

【0014】38は、沈澱分離槽30の外室34より二次中間
水Hを外部に取出す取出パイプで、同取出パイプ38の後
端は、下水道に接続されている。39は沈澱分離槽32の内
部で中間位置に設置するヒーターである。
Reference numeral 38 is a take-out pipe for taking out the secondary intermediate water H from the outer chamber 34 of the precipitation separation tank 30 to the outside, and the rear end of the take-out pipe 38 is connected to the sewer. Reference numeral 39 is a heater installed at an intermediate position inside the precipitation separation tank 32.

【0015】本発明の実施例は上記のように構成されて
おり、レストランなどよりは排出された廃水Aは、ポン
プ手段8によって分離槽2内の分離内槽6に供給され
る。
The embodiment of the present invention is configured as described above, and the waste water A discharged from the restaurant or the like is supplied to the separation inner tank 6 in the separation tank 2 by the pump means 8.

【0016】そして、同分離内槽6に貯溜された廃水A
はヒーター9により加熱され、汚泥物は底部に沈澱して
汚泥物排出パイプ11より外部に排出される。
The wastewater A stored in the separation inner tank 6
Is heated by the heater 9, and sludge is deposited on the bottom and discharged from the sludge discharge pipe 11 to the outside.

【0017】また、廃水A中の油脂成分は上部に浮いた
状態となり、油脂取出管12により濾過槽13の微細目状ス
クリーン14により濾過されて油脂貯溜槽15へ送られる。
Further, the oil and fat component in the wastewater A is floated to the upper part, filtered by the oil and fat take-out pipe 12 by the fine mesh screen 14 of the filter tank 13 and sent to the oil and fat storage tank 15.

【0018】また、分離槽2内にて分離された一次中間
水Dは、分離内槽6の下側開口部5を通って分離外槽4
の外室10に貯溜される。
The primary intermediate water D separated in the separation tank 2 passes through the lower opening 5 of the separation inner tank 6 and the separation outer tank 4
It is stored in the outside room 10 of.

【0019】上記一次中間水Dは、取出口18を通って混
和装置19側へ排出されて、同混和装置19にて、中和剤E
や凝集剤F及び凝集補助剤Gを混和して凝集一次中間水
A-1を供給パイプ19A を介して沈澱分離槽30内へ送り込
む。
The above primary intermediate water D is discharged to the admixing device 19 side through the outlet 18, and in the admixing device 19, the neutralizing agent E is discharged.
Aggregating primary intermediate water by mixing the flocculating agent F and the flocculating aid G
A-1 is sent into the precipitation separation tank 30 via the supply pipe 19A.

【0020】次に、沈澱分離槽30の沈澱分離内槽32に供
給された凝集一次中間水A-1 は、沈澱分離内槽32内にて
沈澱分離されて油脂成分と汚泥及び二次中間水Hとに分
離される。
Next, the coagulated primary intermediate water A-1 supplied to the sedimentation separation inner tank 32 of the sedimentation separation tank 30 is precipitated and separated in the sedimentation separation inner tank 32, and the oil and fat components, sludge and secondary intermediate water are separated. It is separated into H and.

【0021】そして、沈澱分離槽30の外室34に貯溜され
た二次中間水Hは、上澄水としてパイプ38を介して浄水
が排出される。
Then, the secondary intermediate water H stored in the outer chamber 34 of the precipitation separation tank 30 is discharged as purified water via the pipe 38.

【0022】また、沈澱分離槽30内の沈澱分離内槽32に
浮上して貯溜された油脂成分や浮渣44は、油脂戻し管36
を介して分離内槽6へ戻される。
In addition, the oil and fat component and the floating residue 44 which are floated up and stored in the precipitation and separation inner tank 32 in the precipitation and separation tank 30 are stored in the oil and fat return pipe 36.
It is returned to the separation inner tank 6 via.

【0023】以上の如く、上記実施例においては、底部
3を有しタンク状に形成され分離外槽4の内部に、下側
開口部5を有する分離内槽6を位置させて二重構造とし
た分離槽2を設けて、同分離内槽6に、動植物油が混入
された廃水Aを供給して、油脂成分と一次中間水Dとに
分離可能とし、かつ、分離外槽4側より取り出した一次
中間水Dに苛性ソーダなどの中和剤Eを注入混合する混
和装置19を設けると共に、中和剤が混合された凝集中間
水A-1 を沈澱・浮上分離する沈澱分離槽30を設けたもの
であるから、レストランなどから排出される廃水は、同
廃水中に含まれた遊離状態の動植物油や残飯などが二重
構造の分離槽2により確実に分離されて一次中間水が取
り出され、さらに、同一次中間水は、混和装置19におい
ては中和剤などの注入によって沈澱分離槽内での分離が
迅速に、かつ、確実に行われるものである。
As described above, in the above embodiment, the separation inner tank 6 having the bottom portion 3 and formed in the shape of a tank and having the lower opening 5 is positioned inside the separation outer tank 4 to form a double structure. The separation tank 2 is provided, and the waste water A mixed with the animal and vegetable oil is supplied to the separation inner tank 6 so that the oil and fat components and the primary intermediate water D can be separated, and the separation water is taken out from the separation outer tank 4 side. A mixing device 19 for injecting and mixing the neutralizing agent E such as caustic soda into the primary intermediate water D is provided, and a precipitation separating tank 30 for precipitating / floatingly separating the condensed intermediate water A-1 mixed with the neutralizing agent is provided. Therefore, the wastewater discharged from the restaurant, etc. is reliably separated from the free-flowing animal and vegetable oils and leftover food contained in the wastewater by the double-structured separation tank 2 and the primary intermediate water is taken out, In addition, the same intermediate water is injected into the mixing device 19 such as a neutralizing agent. Thus, the separation in the precipitation separation tank can be performed quickly and reliably.

【0024】そして、廃水から油脂成分をとり出して脂
肪酸工業原料としての脂肪酸を容易に製造できるもので
ある。
Then, the fats and oils component can be extracted from the wastewater to easily produce the fatty acid as the raw material for the fatty acid industry.

【0025】また、廃水の処理が連続的に可能であり、
かつ、処理水の質が安定していると共に、処理コストを
節減できるものである。
Further, it is possible to continuously treat wastewater,
Moreover, the quality of the treated water is stable and the treatment cost can be reduced.

【0026】しかも、上記油水分離装置は廃水を自動的
に処理できるから労力が少なくてすみ、また安全であ
る。
In addition, the oil-water separation device can automatically treat wastewater, and thus requires less labor and is safe.

【0027】[0027]

【発明の効果】本発明によれば、底部を有しタンク状に
形成され分離外槽の内部に、下側開口部を有する分離内
槽を位置させて二重構造とした分離槽を設けて、同分離
槽の分離内槽側に、動植物油が混入された廃水を供給し
て、油脂成分と一次中間水とに分離可能とし、かつ、分
離外槽側より取り出した一次中間水に苛性ソーダなどの
中和剤を注入混合する混和装置を設けると共に、中和剤
が混合された凝集中間水を分離する沈澱分離槽を設けた
ものであるから、レストランなどから排出される廃水
は、同廃水中に含まれた動植物油や残飯などが二重構造
の分離槽により確実に分離されて一次中間水が取り出さ
れ、さらに、同一次中間水は、混和装置において中和剤
などの注入によって沈澱分離槽内での分離が迅速に、か
つ、確実に行われるものである。
According to the present invention, a separation tank having a double structure is provided by arranging a separation inner tank having a bottom opening and having a lower opening inside the separation outer tank. By supplying waste water mixed with animal and vegetable oil to the separation inner tank side of the separation tank, it is possible to separate into oil and fat components and primary intermediate water, and caustic soda is added to the primary intermediate water taken out from the separation outer tank side. Since a mixing device for injecting and mixing the neutralizing agent is installed, and a sedimentation separation tank for separating the coagulated intermediate water mixed with the neutralizing agent is installed, the wastewater discharged from the restaurant, etc. The animal and vegetable oils and leftover food contained in the water are reliably separated by the double-structured separation tank, and the primary intermediate water is taken out. In-house separation is fast and reliable Than it is.

【0028】そして、廃水から油脂成分をとり出して脂
肪酸工業原料を容易に製造できるものである。
The fatty acid industrial raw material can be easily produced by removing the fats and oils component from the wastewater.

【0029】また、廃水の処理が連続的に可能であり、
かつ、処理水の質が安定してよくなると共に、処理コス
トを節減できるものである。
Further, it is possible to continuously treat wastewater,
In addition, the quality of treated water is stable and improved, and the treatment cost can be reduced.

【0030】しかも、上記油分離装置は廃水を自動的に
処理できるから労力が少なくてすみ、また安全である。
Moreover, since the oil separation device can automatically treat wastewater, it requires less labor and is safe.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明に係る油水分離装置を示す概略側面図。FIG. 1 is a schematic side view showing an oil / water separator according to the present invention.

【符号の説明】[Explanation of symbols]

A 廃水 A-1 凝集中間水 D 一次中間水 E 中和剤 1 油水分離装置 2 分離槽 3 底部 4 分離外槽 6 分離内槽 30 沈澱分離槽 36 油脂戻し管 A Wastewater A-1 Agglomerated intermediate water D Primary intermediate water E Neutralizer 1 Oil / water separator 2 Separation tank 3 Bottom 4 Separation outer tank 6 Separation inner tank 30 Precipitation separation tank 36 Oil return pipe

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 底部(3) を有しタンク状に形成され分離
外槽(4) の内部に、下側開口部(5) を有する分離内槽
(6) を位置させて二重構造とした分離槽(2) を設けて、
同分離槽(2) の分離内槽(6) 側に、動植物油が混入され
た廃水(A) を供給して、油脂成分と一次中間水(D) 及び
汚泥とに分離可能とし、かつ、分離外槽(4) 側より取り
出した一次中間水(D) に苛性ソーダなどの中和剤(E) を
注入混合する混和装置(19)を設けると共に、中和剤(E)
が混合された凝集中間水(A-1) を油脂成分と浄水とに分
離する沈澱分離槽(30)を設け、しかも、同沈澱分離槽(3
0)には、分離浮上した油脂成分を、分離内槽(6) 側へ返
送する油脂戻し管(36)を具備せしめていることを特徴と
する油水分離装置。
1. A separation inner tank having a bottom (3) and formed in a tank shape, and having a lower opening (5) inside the separation outer tank (4).
A separation tank (2) with a double structure by locating (6) is provided,
Waste water (A) mixed with animal and vegetable oils is supplied to the separation inner tank (6) side of the separation tank (2) to enable separation into oil and fat components, primary intermediate water (D) and sludge, and A mixing device (19) for injecting and mixing the neutralizing agent (E) such as caustic soda into the primary intermediate water (D) taken out from the separation outer tank (4) side is provided, and the neutralizing agent (E)
A precipitation separation tank (30) for separating the coagulated intermediate water (A-1) mixed with water into oil and fat components and purified water is provided.
The oil / water separator according to (0) is equipped with an oil / fat return pipe (36) for returning the separated and floated oil / fat component to the separation inner tank (6) side.
JP4288897A 1992-10-27 1992-10-27 Oil-water separator Expired - Lifetime JP2580449B2 (en)

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JP4288897A JP2580449B2 (en) 1992-10-27 1992-10-27 Oil-water separator

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Application Number Priority Date Filing Date Title
JP4288897A JP2580449B2 (en) 1992-10-27 1992-10-27 Oil-water separator

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JPH06134207A true JPH06134207A (en) 1994-05-17
JP2580449B2 JP2580449B2 (en) 1997-02-12

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001083655A1 (en) * 2000-05-02 2001-11-08 Prolab Technologies Inc. Production of high grade and high concentration of free fatty acids from residual oils, fats and greases
JP2014533194A (en) * 2011-09-29 2014-12-11 キャメロン インターナショナル コーポレイション Equipment for treating interfacial emulsions, water and solids
CN108905290A (en) * 2018-09-25 2018-11-30 江西中医药大学 A kind of tool trap formula oil water separator and volatile oil extracting system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001083655A1 (en) * 2000-05-02 2001-11-08 Prolab Technologies Inc. Production of high grade and high concentration of free fatty acids from residual oils, fats and greases
JP2014533194A (en) * 2011-09-29 2014-12-11 キャメロン インターナショナル コーポレイション Equipment for treating interfacial emulsions, water and solids
US10913013B2 (en) 2011-09-29 2021-02-09 Schlumberger Technology Corporation System and method to process effluent brine and interface rag from an oil dehydration/desalting system
CN108905290A (en) * 2018-09-25 2018-11-30 江西中医药大学 A kind of tool trap formula oil water separator and volatile oil extracting system
CN108905290B (en) * 2018-09-25 2023-09-26 江西中医药大学 Oil-water separator with interception device and volatile oil extraction system

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